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76
CHAPTER 4
1954 Guide
solid and partly broken) of Fig. 6 is found. The maximum value of
may be computed by differentiating w with respect to p and equating the result to zero. This operation produces the formula:
R / 2 \i
(40)
i<
4 i.
"For air, with k = 1.40, -- = 0.53. Pi
Actually, the broken part of the curve is not attained for the flow in the .nozzle. If the ratio of pi to pi is decreased from unity, the mass rate of discharge, as well as the volume, increases from zero to a maximum, as shown by the solid section of the curve in Fig. 6; thereafter, as pi/pi is decreased further, the discharge is constant, as indicated by the horizontal line. The value of pj at the maximum point is called the critical pressure, or Po, and it is seen that p, is approximately 53 percent of pi when air is flowing.
k g
X
I
i
Fig. 6. Relation or Flow or Gas to Pkbssube Drop in a Convebging Tube
I
To find the velocity at the critical pressure, it is assumed that the upstream velocity Vi is so small as to be negligible. Using the subscript c to indicate conditions at the critical point, from Equation 20
Fluid Flow
77
In developing the working equations for orifices and nozzles, it is custom
ary. to start with the incompressible form of the flow Equation 38. In this case both ikf, and Mi are small quantities, .pi = pi, and (pl -- pj)/p> = Ap/pi is small. Retaining only first order terms, it follows from Equation 35 that
so that
Mi At Mt ~ h
(44)
' k-1
1+---W
1 - MS/M,* Vl - (At/A,) , vT
(45)
where 0 _ A/D,. The quantity l/Vl - 0* is the velocity of approach
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0.80,
I
070
O
50.02 Oj
^ " 50lI0D,
w 0.68
oW
030
ilrr
UQ$003 0,--J
0.03 D,
4-IOJ JO4 2
5 10* 2 pV|Di
020 0.10
3 10* 0.03
(O)
Fig. 7. Dimensions and Flow Coefficient for Standard Sharp Edged Orifice
(Coefficient shown as a function of Reynolds Number and Ratio, A/A.)
Note: From Reference 4. Used by permission.
factor as generally used, with 0 being the ratio of the throat or orifice di ameter to the pipe diameter.
Since Ap/p2 is small
Ior
Substituting the critical pressure ratio from Equation 40 it follows that
M,= 1
(43)
or that the velocity at the throat is equal to the local sonic velocity.
and the mass flow is
w = VT^ The volume flow is then
0 = At
V^Zp/p =. At
W7)
]. (48)